Gas diffusion electrode material and production method thereof

ABSTRACT

A gas diffusion electrode material of the present invention includes: a porous body ( 1 ) formed of continuous and discontinuous polytetrafluoroethylene microfibers ( 2 ) and having three-dimensionally continuous micropores ( 4 ); and a conductive material ( 3 ) supported on the porous body ( 1 ). Moreover, a density of the polytetrafluoroethylene microfiber ( 2 ) is lower in a surface region ( 1 A) of a cross section of the porous body ( 1 ) than in an intermediate region ( 1 B) of the cross section. In accordance with the present invention, the polytetrafluoroethylene having the predetermined three-dimensional structure is used, and so on. Therefore, it is possible to provide a gas diffusion electrode material excellent in power generation characteristics and durability.

TECHNICAL FIELD

The present invention relates to a gas diffusion electrode material anda production method thereof, and more specifically, to a gas diffusionelectrode material excellent in power generation characteristics anddurability, to a production method thereof, and to a gas diffusionelectrode.

BACKGROUND ART

Heretofore, in a membrane electrode assembly (MEA) of a solid oxide fuelcell, there has been known a multilayer structure in which electrodestructures (three-phase structures), each being formed of a catalyst inwhich platinum is supported on carbon particles and of ionomer, arebonded to both sides of an electrolyte membrane, and further, gasdiffusion layers are arranged thereon.

For electrode catalyst layers of the three-phase structure, it has beenproposed to enhance drainage thereof by adding a water-repellent agentsuch as polytetrafluoroethylene (PTFE) to the electrode catalyst layers,by using highly hydrophobic carbon black and carbon black subjected tohydrophobic treatment, and so on (refer to Japanese Patent UnexaminedPublication No. S59-43889).

DISCLOSURE OF INVENTION

However, in such conventional electrode catalyst layers of thethree-phase structure, owing to repetition of an operation of the fuelcell, there occur corrosion of the carbon and decomposition anddeterioration of the ionomer, and thus the structure of the electrodecatalyst layers is prone to be deformed/deteriorated. In the electrodecatalyst layers deformed/deteriorated as described above, there has beena problem that gas diffusibility and drainage of generated water aredecreased, resulting in an increase of a concentration overvoltage.

Meanwhile, in an electric vehicle and the like, such a deteriorationfollowing load variations caused by repetition of start and stop thereofis more extensive than in other purposes, and it cannot be said thateven the electrodes described in Japanese Patent Unexamined PublicationNo. S59-43889 are not sufficient yet.

On the other hand, in the solid oxide fuel cell, as such a gas diffusionlayer, heretofore, there has been widely used one, in which carbon paperor carbon cloth is used as a support material, and slurry containing aconductive substance such as the carbon particles and a water-repellentsubstance such as polytetrafluoroethylene (PTFE) is applied on thesupport, whereby a porous layer (a mill layer) is fabricated.

However, in the porous layer (the mill layer) as the gas diffusionlayer, which is as described above, a pore shape and porosity thereofare determined substantially uniquely by amounts of carbon particlespecies and PTFE as constituents. Therefore, when the amount of PTFE isincreased for the purpose of enhancing the drainage, there has been acase where the porosity is decreased, and the gas diffusibility isinhibited. Meanwhile, when the amount of PTFE is reduced for the purposeof enhancing the gas diffusibility, there has been a case where thedrainage becomes worse.

Therefore, there has been proposed a gas diffusion electrode materialthat controls a pore diameter of the porous layer (the mill layer) asthe gas diffusion layer by using two types of carbon materials differentin pore diameter, thereby enhancing the drainage (refer to JapanesePatent Unexamined Publication No. 2001-57215).

However, in the gas diffusion electrode material described in JapanesePatent Unexamined Publication No. 2001-57215, ranges of controllablepore diameter and porosity are narrow, and accordingly, there has been acase where sufficient drainage is not obtained. Moreover, slurrycontaining the carbon particles is applied on an electrode basematerial, the gas diffusion electrode is thereby fabricated, andaccordingly, there has been a case where the carbon particles areadhered into pores of the base material, and the pores of the basematerial are filled therewith, whereby gas permeability is significantlydecreased.

The present invention has been made in consideration for the problems asdescribed above, which are inherent in the conventional technologies. Itis an object of the present invention to provide a gas diffusionelectrode material excellent in power generation characteristics anddurability, a production method thereof, and a gas diffusion electrode.

A gas diffusion electrode material according to a first aspect of thepresent invention includes: a porous body formed of continuous anddiscontinuous polytetrafluoroethylene microfibers and havingthree-dimensionally continuous micropores; and a conductive materialsupported on the porous body, wherein a density of thepolytetrafluoroethylene microfiber is lower in a surface region of across section of the porous body than in an intermediate region of thecross section.

A method for producing a gas diffusion electrode material according to asecond aspect of the present invention includes the steps of:hydrophilizing a porous body formed of continuous and discontinuouspolytetrafluoroethylene microfibers and having three-dimensionallycontinuous micropores; impregnating and adhering slurry containing aconductive material into and onto the hydrophilized porous body; andperforming heat treatment for the porous body onto which the conductivematerial is adhered.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 is electron microscope photographs of a porous body in an exampleof a gas diffusion electrode material of the present invention.

FIG. 2 is electron microscope photographs of an example of the gasdiffusion electrode material of the present invention.

FIG. 3 is electron microscope photographs of a porous body in aconventional gas diffusion electrode material.

FIG. 4 is electron microscope photographs of the conventional gasdiffusion electrode material.

FIG. 5 is a process flowchart showing an example of a production methodof the gas diffusion electrode material of the present invention.

FIG. 6 is a schematic cross-sectional view showing an example of a gasdiffusion electrode using the gas diffusion electrode material of thepresent invention.

FIG. 7 is a schematic cross-sectional view showing an example of asingle cell using the gas diffusion electrode material of the presentinvention.

FIG. 8A is a table showing configurations and evaluation results ofexamples and comparative examples.

FIG. 8B is a table showing the configurations and evaluation results ofthe examples and the comparative examples.

BEST MODE FOR CARRYING OUT THE INVENTION

A description will be made below in detail of embodiments of a gasdiffusion electrode material of the present invention and a productionmethod thereof based on the drawings. Note that, in this specification,“%” denotes a mass percent unless otherwise specified.

The gas diffusion electrode material of the present invention includes:a porous body formed of continuous and discontinuouspolytetrafluoroethylene microfibers; and a conductive material supportedon the porous body.

The porous body is formed of the polytetrafluoroethylene microfiber, andhas three-dimensionally continuous micropores. Then, the conductivematerial is contained mainly in the three-dimensionally continuousmicropores.

Here, the polytetrafluoroethylene (PTFE) fiber is electricallyinsulative; however, as described above, the conductive material iscontained in the porous body made of the PTFE microfiber, wherebyconduction routes can be formed in the porous body. Therefore, theporous body becomes one usable as the gas diffusion electrode material,and typically, functions as a porous layer (a mill layer) of a gasdiffusion electrode.

Moreover, in the gas diffusion electrode material of the presentinvention, when a cross section of the above-described porous body isobserved, the continuous and discontinuous PTFE microfibers havelow-density regions and high-density regions from a front surface regionto a back surface region. As a typical distribution (gradient) of thedensity, for example, the density of the PTFE microfiber can be set soas to be from high to low from the front surface region to the backsurface region, and to be from low through high to low and from highthrough low to high from the front surface region through anintermediate region to the back surface region.

FIG. 1 is electron microscope photographs of the above-described porousbody in an example of the gas diffusion electrode material of thepresent invention: FIG. 1A shows a part of the front surface region ofthe cross section of the porous body; and FIG. 1B shows a part of theintermediate region thereof. As apparent from FIGS. 1A and 1B, in theintermediate region of a porous body 1, PTFE microfiber 2 is densifiedmore than in the front surface region. Note that, though the crosssection in the back surface region of the porous body is not shown inFIG. 1, a state of the cross section in the back surface region issubstantially the same as a state of the cross section of the frontsurface region.

Moreover, in the gas diffusion electrode material of the presentinvention, when a cross section thereof is observed, a degree ofsupporting the above-described conductive material can be increased inthe region where the density of the PTFE microfiber is low, and thedegree of supporting the conductive material can be decreased in theregion where the density of the PTFE microfiber is high.

A typical distribution (gradient) of the degree of supporting theconductive material can be set so as to be from low to high (so as tohold the conductive material only on one surface) when the density ofthe PTFE microfiber is from high to low from the front surface region tothe back surface region. Moreover, the distribution of the degree ofsupporting the conductive material can be set so as to be from highthrough low to high (so as to hold the conductive material on bothsurfaces) when the density of the PTFE microfiber is from low throughhigh to low from the front surface region through the intermediateregion to the back surface region.

FIG. 2 is electron microscope photographs of an example of a gasdiffusion electrode material 10 of the present invention. Here, thephotographs are ones obtained by observing a cross section of the gasdiffusion electrode material 10 that forms a sheet shape.

As shown in FIG. 2, owing to the density of the PTFE microfiber in theabove-described porous body, particles 3 of the conductive material areheld more in a front surface region 1A (refer to FIG. 2(A)) of theporous body 1 than in an intermediate region 1B (refer to FIG. 2(B))thereof.

By the distribution of the conductive material, which is as describedabove, in the gas diffusion electrode material of the present invention,adhesion on an interface thereof with an electrode catalyst layerbecomes good. Therefore, in an area from the electrode catalyst layer onan electrolyte membrane to a support material such as carbon paper,diffusibility and movement of gas and liquid components become suitableones. Moreover, by the distribution, flooding under a high humiditycondition is suppressed. Furthermore, start-stop durability and opencircuit voltage (OCV) durability, which are for accelerating thedrainage in the electrode catalyst layer, are also enhanced. Stillfurther, movement of water held in the electrolyte membrane under a lowhumidity condition is also facilitated, and high power generationperformance is obtained.

Moreover, by the distribution of the conductive material, which is asdescribed above, in the gas diffusion electrode material of the presentinvention, adhesion thereof onto the support material is good in thecase of using the support material such as the carbon paper, and the gasdiffusion electrode material becomes one excellent in durability againstexternal force. Therefore, the gas diffusion electrode material becomesa particularly suitable one to be mounted on an automobile subjectedrepeatedly to long-time vibrations when an engine starts, the automobileruns, and so on.

Note that, as shown in FIG. 1, the porous body made of the PTFEmicrofiber, which is used for the gas diffusion electrode material ofthe present invention, typically has slit-like three-dimensionally (3D)continuous micropores 4.

As will be described later, the 3D continuous micropores are ones causedby a production process of the porous body. By the fact that the porousbody has such micropores, the gas diffusion electrode material of thepresent invention realizes a diffusion electrode structure in whichporosity is high, and suppresses the flooding under the high humiditycondition. Moreover, since the drainage in the electrode catalyst layeris accelerated, the start-stop durability and the OCV durability arealso enhanced. Furthermore, the movement of the water held in theelectrolyte membrane under the low humidity condition is alsofacilitated, the gas diffusion electrode material is able to exert afunction that the high power generation performance is obtained.

Moreover, a fiber diameter of the PTFE microfiber is not particularlylimited; however, typically, is approximately 0.1 to 5 μm.

Furthermore, it is preferable that, in the gas diffusion electrodematerial of the present invention, a mass ratio of thepolytetrafluoroethylene and the conductive material satisfy arelationship represented by the following Formula

(PTFE): (Conductor)=20 to 80: 80 to 20  (1)

(where PTFE is the polytetrafluoroethylene, and Conductor is theconductive material).

As described above, the porous body made of the PTFE microfiber isallowed to hold the conductive material, for example, the carbonparticles, whereby the conduction routes are formed in the porous body,and the porous body becomes able to function as the mill layer for thegas diffusion electrode. However, on the contrary, when the conductivematerial is excessively filled into the pores of the porous body, thereis a case where gas routes are narrowed to decrease gas permeability. Inconsideration for this point, it is preferable that the gas diffusionelectrode material satisfy the relationship of the above-describedFormula (1). Note that, in the above-described Formula (1), when acontent of the conductive material is less than 20%, there is a casewhere the conductivity cannot be ensured sufficiently, and when thecontent exceeds 80%, there is a case where the gas permeability(diffusibility) and water repellency become insufficient.

Note that, in the gas diffusion electrode material of the presentinvention, water is less likely to enter an inside thereof and is likelyto be drained even if entering the inside since the porous body itselfis formed of the PTFE fiber having high water repellency. Hence, such aconfiguration of the present invention also contributes to moistureremoval from the electrode catalyst layer with which the gas diffusionelectrode material (the mill layer) will be brought into contact.

Moreover, since the porous body as described above has the 3D continuousmicropores, the gas diffusion electrode material of the presentinvention is also excellent in physical characteristics such ascompressive strength, heat resistance and durability.

Here, in general, in the gas diffusion electrode, the slurry containingcarbon black and PTFE is applied on the surface of the carbon paper orthe carbon cloth, which serves as the support material, followed byheating, whereby the mill layer is formed. In this case, carbonaggregates in the slurry have a size of several 100 nm to 1 μm.Accordingly, a size of the micropores formed in the mill layer after thecarbon black is supported is mostly several 100 nm to 1 μm, and porosityin the mill layer also becomes approximately 20 to 50%. Hence, unlikethe gas diffusion electrode material of the present invention, in themill layer of the usual gas diffusion electrode, gas permeability(diffusibility) thereof is insufficient in comparison with that in thesupport material such as the carbon paper, and further, such moistureremoval from the electrode catalyst layer in contact with the mill layeralso becomes prone to be insufficient.

Note that there are various forms of the porous bodies, typically,porous membranes; however, one excellent in gas diffusibility and waterrepellency is suitable for use as a base material of the gas diffusionelectrode material.

Moreover, the gas diffusibility of the porous membrane (the porous body)as described above is affected by a membrane thickness thereof, theporosity and the pore diameter. In the present invention, preferably,the thickness is 5 to 50 μm, the porosity is 70% or more, and the porediameter is 0.5 to 45 μm. In such a way, suitable gas diffusibility canbe ensured.

Moreover, in the gas diffusion electrode material of the presentinvention, which is composed by holding the conductive material on theabove-described porous body, preferably, the porosity is 40 to 85%, andthe pore diameter is 1 to 30 μm. In order to ensure sufficient gasdiffusibility as the gas diffusion electrode material after holding theconductive material in the porous body, it is preferable that the gasdiffusion electrode material have the above-described characteristics.

Note that, in the present invention, it is sufficient if theabove-described conductive material is particles having electricconductivity; however, typically, it is desirably to use carbon black inwhich a particle diameter (D50) is 0.5 to 2 μm, preferably, 0.5 to 1.5μm, and more preferably, 0.9 to 1.0 μm. When the particle diameter issmaller than 0.5 μm, the conductive material sometimes passes throughthe 3D continuous micropores of the above-described porous body even ifthe conductive material can enter the same. Meanwhile, when the particlediameter exceeds 2 μm, the conductive material cannot sometimes enterthe 3D continuous micropores, and the conduction routes cannot sometimesbe formed in the porous body.

Moreover, in order to ensure the water repellency of the gas diffusionelectrode for which the carbon black is to be used, preferably, thecarbon black is one in which a specific surface area is 30 to 2000 m²/g.In particular, acetylene black or graphitized carbon black is suitable,in which a specific surface area is 30 to 900 m²/g, an average latticespacing d002 on a (002) plane in X-ray diffraction is 0.343 to 0.362 nm.

Note that, in order to ensure the water repellency of the gas diffusionelectrode for which the gas diffusion electrode material of the presentinvention is to be used, besides the conductive material, componentssuch as a PTFE dispersion as a water-repellent agent can be added to thegas diffusion electrode material.

Moreover, it is preferable that an amount of a solid content includingthe conductive material and these additional components be set at 0.5 to3.0 mg/cm² per unit area of the above-described porous body made ofPTFE. When the amount of the solid content is less than 0.5 mg/cm², theconduction routes are sometimes formed insufficiently, and when theamount of the solid content exceeds 3.0 mg/cm², the gas diffusibility issometimes decreased.

Next, a description will be made of another gas diffusion electrodematerial of the present invention.

This gas diffusion electrode material of the present invention has asubstantially similar configuration to that of the above-described gasdiffusion electrode material; however, is different therefromparticularly in the following point.

Specifically, this gas diffusion electrode material is composed byallowing the slit-like three dimensionally continuous micropores formedin the porous body to contain at least the conductive material. Thisporous body is formed of either one or both of continuous microfiber anddiscontinuous microfiber, which are obtained by uniaxially or biaxiallystretching a thin membrane made of polytetrafluoroethylene.

Moreover, in this gas diffusion electrode material, a mass ratio of thepolytetrafluoroethylene and the conductive material satisfies arelationship represented by the following Formula (2):

(PTFE): (Conductor)=20 to 60: 80 to 40  (2)

(where PTFE is the polytetrafluoroethylene, and Conductor is theconductive material).

Here, the porous body made of the polytetrafluoroethylene is a basematerial that is insulative and has continuous micropores. In order touse this porous body as the gas diffusion electrode material (the porouslayer (the mill layer) of the GDL), it is necessary to form theconduction routes by allowing the porous body to contain the conductivematerial. Meanwhile, when the conductive material is contained in gaps(pores) of the porous body, there is a case where gaps of the basematerial are filled therewith, and gap routes are narrowed, whereby thegas permeability is significantly decreased.

Therefore, in the present invention, the gas diffusion electrodematerial is set so as to satisfy the above-described Composition Formula(2), whereby the conductivity, which is provided in the conductivematerial, and the gas permeability and the water repellency, which areprovided in the porous body, are made compatible with each other.

Note that, when a content of the conductive material is less than 40%,the conductivity cannot be ensured sufficiently. Meanwhile, when thecontent of the conductive material exceeds 80%, the gap routes arenarrowed, whereby the gas permeability is prone to be decreasedsignificantly.

Moreover, in order to use the above-described porous body as the basematerial of the gas diffusion electrode material (the porous layer (themill layer) of the GDL), it is recommended that the porous body be onehaving excellent gas diffusibility (gas permeability) and high waterrepellency. The gas diffusibility can be ensured by adjusting themembrane thickness, the porosity and the pore diameter. For example, itis preferable to use a porous body in which the thickness is 5 to 50 theporosity is 80% or more, the pore diameter is 0.5 to 45 μm, and the gaspermeability is 1 to 30 L/min·cm². For example, one having physicalproperty values equivalent to the above, which is selected from amongporous membranes such as Poreflon Membrane (article name; made bySumitomo Electric Fine Polymer, Inc), can be suitably used.

In this case, good gas diffusibility can be ensured even after carbonparticles, in which a particle diameter (D50) is 0.1 μm to 10 μminclusive (in which a particle diameter of aggregates of primaryparticles is 10 μm or less), are contained as the conductive material.Note that, since the porous body is made of the polytetrafluoroethylene,the water repellency thereof is high.

Moreover, as the conductive material for forming the conduction routesby being contained in the pores of the porous body, carbon black(including aggregates thereof) can be used, in which a particle diameter(D50) is 0.01 to 2 μm, and a specific surface area is 30 to 2000 m²/g.For example, AB-6 (acetylene black; specific surface area of 40 m²/g;made by Denki Kagaku Kogyo Kabushiki Kaisha) can be suitably used. Useof the conductive material as described above is effective since theconductive material can be dispersed uniformly and highly into thepores.

Note that, when the particle diameter of the conductive material exceeds2 μm, there is a case where the conductive material particles are hookedon the pores of the porous membrane, and the conduction routes are notformed well. Note that the pores mentioned here do not show a shape inwhich a round hole is open, but show a shape of a slit-like crack formedin such a manner that a part of the PTFE membrane is torn off.

In such a gas diffusion electrode material, it is suitable that, afterthe conductive material is supported therein, the porosity be 40 to 80%,the pore diameter be 1 to 30 μm, and the gas permeability be 1 to 20L/min·cm², from a viewpoint of ensuring the gas diffusibility.

Moreover, it is desirable that an adhered amount (the amount of solidcontent) of the conductive material be within a range of 0.3 to 3.0mg/cm² per unit area of the polytetrafluoroethylene serving as the basematerial. When the adhered amount is less than 0.3 mg/cm², theconduction routes become prone to be formed insufficiently. When theadhered amount exceeds 3.0 mg/cm², the gas diffusibility is sometimesdecreased.

Next, a description will be made of the production method of the gasdiffusion electrode material of the present invention.

This production method is a method for producing the above-described gasdiffusion electrode material of the present invention, which includesthe following steps (1) to (3):

(1) the step of hydrophilizing a porous body formed of continuous anddiscontinuous polytetrafluoroethylene microfibers and havingthree-dimensionally continuous micropores;

(2) the step of impregnating and adhering slurry containing a conductivematerial into and onto the hydrophilized porous body; and

(3) the step of performing heat treatment for the porous body onto whichthe conductive material is adhered.

It is preferable that a polytetrafluoroethylene membrane for use in thestep (1) be fabricated by being subjected to uniaxial or biaxialstretching. By such stretching treatment for the PTFE, the slit-like 3Dcontinuous micropores are formed.

Moreover, the step (1) is performed in order to facilitate thesubsequent impregnation and adhesion (the step (2)) of the slurry(ink-like aqueous slurry) in consideration for the high water repellencyof the PTFE.

Specifically, such a step (1) is performed by allowing surfactant to becontained in the three-dimensionally continuous micropores of theabove-described porous body, and filling an organic solvent havinghydrophilic groups.

In this case, as the organic solvent, one having hydrophilic groups(typically, hydroxyl groups) and lipophilic groups, for example, alcoholin which a boiling point is 50 to 150° C., is preferable. Ethanol(boiling point: 78.5° C.), propanol (boiling point: 97° C.), butanol(boiling point: 108.1° C.) and hexanol (boiling point: 136° C.) can bementioned.

Moreover, as the surfactant for use, there can be mentioned Triton X-100(article name), Naroacty HN-100 (article name), nonionic surfactant(ether type), and the like.

Next, the step (2) is one performed in order to allow conductiveparticles in the slurry containing the conductive material, typically,carbon particles to enter the 3D continuous micropores of theabove-described porous body.

Specifically, the step (2) is performed in the following manner. Theabove-described slurry is brought into contact with either a frontsurface or back surface of the above-described porous body, andthereafter, the porous body is pressurized or decompressed, whereby theslurry is impregnated into the inside of the porous body. Subsequently,the surfactant and the organic solvent in the slurry are dried under anormal atmospheric pressure, and the conductive material is fixed to theporous body.

As described above, the hydrophilizing treatment (the step (1)) and theimpregnation/adhesion of the slurry (the step (2)) are performed inwet-to-wet fashion, thus making it possible to uniformly impregnate suchconductive material-containing slurry into the porous body. In such away, the adhered amount of the slurry can be controlled withinvariations of up to +10% with respect to a target amount.

Moreover, preferably, the hydrophilizing treatment is performed for bothsurfaces of the porous body in the step (1), and the conductive materialcontaining-slurry is impregnated and adhered into and onto thethree-dimensionally continuous micropores of the porous body from bothsurfaces of the porous body in the step (2). Specifically, thehydrophilizing treatment is performed for one surface of the porousbody, and the conductive material-containing slurry is adheredthereonto, and moreover, the hydrophilizing step and the slurry adheringstep are performed in similar way also on the other surface. Moreover,the following procedure may be performed, in which the hydrophilizingtreatment is performed for both surfaces of the porous body, theconductive material-containing slurry is adhered onto one surface of theporous body, and such a slurry adhering step is then performed in asimilar way also for the other surface.

In this case, the conductivity of the porous body containing theconductive material is likely to be enhanced, and can be set at 10mΩ·cm² or less. Note that, in the case of only the slurry impregnationfrom one surface, the polytetrafluoroethylene fiber of the porous bodyis sometimes exposed to the other surface, resulting in the decrease ofthe conductivity.

Moreover, the step (3) is one performed in order to fix the conductivematerial contained in the porous body.

In this step, the porous body is heated up to a temperature equal to orhigher than a melting point of the PTFE as the porous body, whereby theconductive material is fixed to the porous body. In usual, the meltingpoint of the PTFE is approximately 320° C., and a melting point of theporous body becomes approximately 300 to 350° C. Hence, it is preferableto perform such heat treatment at 300 to 400° C. When such a heattreatment temperature is lower than 300° C., there is a case where theporous body is not molten, and the conductive material particles cannotbe fixed to the porous body. When the heat treatment temperature exceeds400° C., there is a case where the melting of the porous body advancestoo much, and deformation such as breakage is caused in the 3Dcontinuous micropores, resulting in the decrease of the gasdiffusibility.

Moreover, in the step (3), it is preferable to perform the heattreatment for the porous body, onto which the conductive material isadhered, in a state where tension is applied thereto in a directionparallel to the surface thereof. As described above, when the heattreatment is performed for the porous body made of the PTFE, there is acase where, owing to the melting of the PTFE, a volume of the porousbody is shrunken, and the 3D continuous micropores are narrowed.Consequently, the gas diffusibility is sometimes decreased. As opposedto this, when the heat treatment is performed in a state where thetension is applied to the porous body in the direction parallel to thesurface direction, for example, in two directions (X-Y directions)perpendicular to each other, such a malfunction can be suppressed.

Note that the heat treatment may be performed while leaving the porousbody fixed to formworks besides applying the tension thereto.

FIG. 5 shows an example of a process flow of manufacturing the gasdiffusion electrode using the gas diffusion electrode material of thepresent invention through the above-described steps (1) to (3). In thisprocess flow, first, the porous body (the porous PTFE sheet) 1 is fixedby formworks 5 a and 5 b. Thereafter, the porous body 1 is allowed tocontain the surfactant, is filled with the organic solvent, and isdecompressed from a lower surface thereof, whereby the hydrophilizingtreatment is performed therefor (the step (1)). Moreover, after the step(1), the conductive material-containing slurry is applied on thehydrophilized porous body. Thereafter, the porous body 1 is decompressedfrom the lower surface thereof, whereby the above-described slurry isimpregnated into the inside of the porous body 1. Thereafter, the porousbody 1 is dried under the normal atmospheric pressure in a continuousdrying furnace, whereby the conductive material is adhered onto theporous body (the step (2)). After the step (2), the formworks 5 a and 5b are detached from the porous body 1 on which the conductive materialis adhered, and the porous body 1 is subjected to the heat treatment ina continuous heating furnace, whereby the conductive material is fixedto the porous body 1 (the step (3)). After the step (3), the completedgas diffusion electrode material is put into a press machine togetherwith a support material 6, and the gas diffusion electrode material andthe support material are bonded to each other, followed by cutting,whereby the gas diffusion electrode can be obtained. Note that, afterthe step (1) and the step (2) are performed, the porous body 1 is turnedupside down, and the same steps are repeatedly performed for the backsurface, whereby the conductive material is impregnated/adheredinto/onto the porous body I from both surfaces thereof. In such a way,the gas diffusion electrode material can be manufactured.

Next, a description will be made of the electrode catalyst layer of thegas diffusion electrode of the present invention.

The electrode catalyst layer of the present invention is one composed bysupporting an electrode catalyst on the above-described gas diffusionelectrode material of the present invention.

As such an electrode catalyst, there can be mentioned catalysts in whichthe following active components are supported on a conductive material(a carbon support). The active components are such as: platinum (Pt),palladium (Pd), rhodium (Rh), iridium (Ir), ruthenium (Ru), or Pt alloyscontaining mixtures of theses; and cobalt (Co), iron (Fe), nickel (Ni),chromium (Cr), manganese (Mn), or Pt alloys containing mixtures ofthese.

Next, a description will be made of the gas diffusion electrode of thepresent invention.

As shown in FIG. 5, the gas diffusion electrode of the present inventionis composed by supporting the above-described gas diffusion electrodematerial or electrode catalyst layer of the present invention by thegas-permeable conductive support material 6 such as the carbon paper andthe carbon cloth.

The gas diffusion electrode material of the present invention can bedirectly used as the gas diffusion electrode; however, if the gasdiffusion electrode material is supported by the carbon paper and thelike, then rigidity thereof can be enhanced, and handling easinessthereof can be further enhanced.

As such a conductive support material, one with a thickness of 100 to300 μm is preferable. When the thickness is less than 100 μm, strengththereof sometimes becomes insufficient, and when the thickness exceeds300 μm, the gas diffusibility is sometimes inhibited.

Moreover, it is sufficient if the carbon paper and the carbon cloth haveconductivity, and graphitization degrees thereof may be low.

Note that, though water repellent treatment is performed for the carbonpaper and the carbon cloth in the conventional gas diffusion electrode,such water repellent treatment is unnecessary in the present invention.The carbon paper and the like are sometimes deteriorated following atime deterioration of a water repellent for use in the water repellenttreatment, and accordingly, it is recommended that the water repellenttreatment would not rather be performed in the present invention.

It is as described above that the gas diffusion electrode material ofthe present invention can be used as the gas diffusion layer even ifbeing left fixed to the support material such as the carbon paper andthe carbon cloth. Moreover, as shown in FIG. 6, in the case where a gasdiffusion electrode 9 is composed by supporting the gas diffusionelectrode material 10 of the present invention on an electrode catalystlayer 8 provided on an electrolyte membrane 7, adhesion between theelectrode catalyst layer 8 and the gas diffusion electrode material 10can be enhanced, contact resistance therebetween can be reduced, and thepower generation performance of the gas diffusion electrode material canbe further enhanced.

A description will be made below more in detail of the present inventionby examples and comparative examples; however, the present invention isnot limited to these examples.

EXAMPLE 1

Fabrication procedures of the gas diffusion electrode material and theMEA will be described below.

[Fabrication of Gas Diffusion Electrode] 1. Preparation ofPolytetrafluoroethylene Porous Membrane

A base material with a size of 10 cm square was cut out of the slit-likepolytetrafluoroethylene porous membrane sheet shown in FIG. 1, in whichthe thickness was 30 μm, the pore diameter ranged from 0.5 to 45 μm (theaverage pore diameter: 15 μm), and the porosity was 88%.

2. Preparation of Hydrophilizing Treatment Solution

4 g of the surfactant (Triton X-100 made by The Dow Chemical Company)and 200 g of ethanol were mixed together, and a resultant solution wassubjected to stirring/dispersion treatment for 30 minutes at 150 rpm ina propeller stirrer, and was formed into a hydrophilizing treatmentsolution.

3. Preparation of Coating Ink Slurry

3 g of the surfactant (Triton X-100 made by The Dow Chemical Company)and 200 g of pure water were mixed together, and a resultant solutionwas subjected to stirring treatment for 30 minutes at 150 rpm in thepropeller stirrer. Thereafter, 20 g of the acetylene black (AB-6) madeby Denki Kagaku Kogyo Kabushiki Kaisha was put into and mixed with theabove-described surfactant-dispersed solution, and a resultant mixturewas subjected to stirring treatment for 30 minutes at 150 rpm in thepropeller stirrer.

The above-described ink slurry was subjected to milling treatment byusing a jet mill, and an average particle diameter of carbon thereof wasset at 1 3 g of Polyflon D-1E (solid content: 64%) made by DaikinIndustries, Ltd. was put into and mixed with the above-described inkslurry. Then, a resultant mixture was subjected to stirring treatmentfor 30 minutes at 150 rpm in the propeller stirrer, whereby coating inkslurry was formed.

4. Hydrophilizing Treatment (1)

The base material cut out into the size of 10 cm square was fixed to astainless steel-made jig in which a hollow portion had a size of 8 cmsquare, and was placed on a decompression/suction plate. 25 ml of thehydrophilizing treatment solution was immersed entirely into one surfaceof the base material, and was decompressed and sucked, whereby thehydrophilizing treatment solution was impregnated into the basematerial. Subsequently, such a decompression/suction operation wasstopped in a state where the hydrophilizing treatment solution wasimpregnated sufficiently into the base material, whereby a state wasbrought, in which the hydrophilizing treatment solution was filled intothe base material.

5. Coating Treatment (1)

In the state where the hydrophilizing treatment solution was filled intothe base material, 15 ml of the above-described prepared coating inkslurry was immersed into the base material, followed by decompressionand suction, whereby the coating ink slurry was impregnated into thebase material while being substituted for the hydrophilizing treatmentsolution in the base material. After the ink slurry was sufficientlyimpregnated, a resultant of the above was dried for 15 minutes in adrying furnace (at the air atmosphere) at 80° C. In such a way, a basematerial al of which one surface was subjected to the treatment wasobtained.

6. Hydrophilizing Treatment (2)

Next, in order to treat an untreated surface of the base material a1,the base material a1 was fixed to the stainless steel-made jig in whichthe hollow portion had a size of 8 cm square, and was placed on thedecompression/suction plate in a similar manner to the above. 25 ml ofthe hydrophilizing treatment solution was immersed entirely into theother surface of the base material, followed by decompression andsuction, whereby the hydrophilizing treatment solution was impregnatedinto the base material.

Subsequently, such a decompression/suction operation was stopped in astate where the hydrophilizing treatment solution was impregnatedsufficiently into the base material, whereby a state was brought, inwhich the hydrophilizing treatment solution was filled into the basematerial.

7. Coating Treatment (2)

In the state where the hydrophilizing treatment solution was filled intothe base material, 15 ml of the above-described prepared coating inkslurry was immersed into the base material, followed by decompressionand suction, whereby the coating ink slurry was impregnated into thebase material while being substituted for the hydrophilizing treatmentsolution in the base material. After the ink slurry was sufficientlyimpregnated, a resultant of the above was dried for 15 minutes in thedrying furnace (at the air atmosphere) at 80° C. In such a way, a basematerial a2 of which both surfaces were subjected to the treatment wasobtained. A total coated amount of a solid content of the ink slurry onthe base material a2 was 1.0 mg/cm².

8. Heating of Porous Membrane

The base material a2 in which the ink slurry was coated on both surfaceswas subjected to heat treatment for 10 minutes in a heating furnace (atthe air atmosphere) at 350° C., and PTFE-dispersed particles containedin the base material and the PTFE fiber of skeletons thereof were moltentogether. In such a way, the PTFE was dispersed onto the carbonparticles contained in the base material, and the gas diffusionelectrode material was formed. In such a way, the gas diffusionelectrode material A1 shown in FIG. 2 was obtained, in which the massratio of (PTFE): (Conductor) was equal to 30:70, and the porosity was70%.

9. Bonding of Carbon Paper

The above-described gas diffusion electrode material Al was set oncarbon paper named TGP-H-060 made by Toray Industries, Inc., which had asize of 10 cm square, and the gas diffusion electrode material and thecarbon paper were subjected to bonding treatment for three minutes at130° C. and 2 MPa by hot press.

A bonded body of the carbon paper and the gas diffusion electrodematerial A1, which was thus obtained, was cut out into a predeterminedsize (6.0 cm×5.5 cm), and a gas diffusion electrode G1 was formed.

[Fabrication of Membrane Electrode Assembly (MEA)] 1. Preparation ofAnode Electrode Catalyst

As the conductive carbon material, 4.0 g of carbon black (Ketjen Black™EC made by Ketjen Black International Company, BET specific surfacearea: 800 m²/g) was prepared. To this conductive carbon material, addedwas 400 g of a dinitrodiammine platinum solution (Pt concentration:1.0%), and a resultant solution was stirred for one hour. Moreover, 50 gof methanol was mixed as a reducing agent to the solution, and aresultant solution was stirred for one hour. Thereafter, the solutionwas heated up to 80° C. for 30 minutes, was stirred at 80° C. for sixhours, and was then cooled down to room temperature for one hour.

After a deposition was filtered, a solid material thus obtained wasdried at 85° C. under a reduced pressure for 12 hours, and was milled ina mortar, whereby an anode electrode catalyst (average particle diameterof Pt particles: 2.6 nm; supported concentration of Pt: 50 mass %) wasobtained.

2. Preparation of Cathode Electrode Catalyst

The carbon black (Ketjen Black™ EC made by Ketjen Black InternationalCompany) was subjected to heat treatment, whereby carbon black(graphitized Ketjen Black EC, BET specific surface area: 130 m²/g)subjected to graphitization treatment was obtained. 400 g of adinitrodiammine platinum solution (Pt concentration: 1.0%) was added to4.0 g of the Ketjen Black thus subjected to the graphitizationtreatment, and a resultant solution was stirred for one hour. Moreover,50 g of formic acid was mixed as a reducing agent to the solution, and aresultant solution was stirred for one hour. Thereafter, the solutionwas heated up to 40° C. for 30 minutes, and was stirred at 40° C. forsix hours. Moreover, the solution was heated up to 60° C. for 30minutes, further, was stirred at 60° C. for six hours, and was thencooled down to the room temperature for one hour. After a deposition wasfiltered, a solid material thus obtained was dried at 85° C. under areduced pressure for 12 hours, and was milled in the mortar, whereby acathode electrode catalyst (average particle diameter of Pt particles:4.8 nm; supported concentration of Pt: 50 mass %) was obtained.

3. Fabrication of Anode Catalyst Layer

Purified water of which amount was five times a mass of the anodeelectrode catalyst was added thereto, and a resultant solution wassubjected to a decompression/deaerating operation for five minutes.n-propyl alcohol of which amount was 0.5 time an amount of the solutionwas added thereto, and further, a solution (containing 20% Nafion madeby DuPont Corporation) containing a proton-conductive polymerelectrolyte was added thereto. As the polymer electrolyte in thesolution, one was used, in which a solid mass ratio of a content withrespect to the carbon of the anode electrode catalyst, that is,Carbon/Ionomer was equal to 1.0/0.9.

Mixed slurry thus obtained was dispersed well by an ultrasonichomogenizer, and was subjected to the decompression/deaeratingoperation, whereby catalyst slurry was prepared. This catalyst slurry ofwhich amount corresponded to the desired thickness was printed on onesurface of a polytetrafluoroethylene sheet by a screen printing method,and was dried at 60° C. for 24 hours. A size of the formed anodecatalyst layer was set at 5 cm×5 cm. Moreover, the coated layer on thepolytetrafluoroethylene sheet was adjusted so that an amount of Pt couldbe 0.2 mg/cm² (average thickness of the anode catalyst layer: 6 μm).

4. Fabrication of Cathode Catalyst Layer

Purified water of which amount was five times a mass of the cathodeelectrode catalyst was added thereto, and a resultant solution wassubjected to the decompression/deaerating operation for five minutes.n-propyl alcohol of which amount was 0.5 time an amount of the solutionwas added thereto, and further, a solution (containing 20% Nafion madeby DuPont Corporation) containing the proton-conductive polymerelectrolyte was added thereto. As the polymer electrolyte in thesolution, one was used, in which a solid mass ratio of a content withrespect to the carbon of the cathode electrode catalyst, that is,Carbon/Ionomer was equal to 1.0/0.9.

Mixed slurry thus obtained was dispersed well by the ultrasonichomogenizer, and was subjected to the decompression/deaeratingoperation, whereby catalyst slurry was prepared. This catalyst slurry ofwhich amount corresponded to the desired thickness was printed on theother surface of the polytetrafluoroethylene sheet by the screenprinting method, and was dried at 60° C. for 24 hours. A size of theformed cathode catalyst layer was set at 5 cm×5 cm. Moreover, the coatedlayer on the polytetrafluoroethylene sheet was adjusted so that anamount of Pt could be 0.4 mg/cm² (average thickness of the cathodecatalyst layer: 12 μm).

5. Fabrication of Membrane Electrode Assembly (MEA)

Nafion™ NRE211 (the former NE111) (membrane thickness: 25 μm), whichserved as a solid polymer electrolyte membrane, and the electrodecatalyst layers formed on the polytetrafluoroethylene sheets, which werefabricated in advance, were superposed on one another. In this case, theanode catalyst layer, the solid polymer electrolyte membrane and thecathode catalyst layer were stacked on one another in this order.Thereafter, this body thus stacked was hot-pressed at 130° C. and 2.0MPa for 10 minutes, and only the polytetrafluoroethylene sheets werepeeled therefrom, whereby an MEA was obtained.

With regard to the cathode catalyst layer transferred onto the solidpolymer electrolyte membrane, the thickness was approximately 12 μm, thesupported amount of Pt was 0.4 mg per 1 cm² of an apparent electrodearea, and the electrode area was 25 cm². With regard to the anodecatalyst layer, the thickness was approximately 6 μm, the supportedamount of Pt was 0.2 mg per 1 cm² of an apparent electrode area, and theelectrode area was 25 cm².

[Performance Evaluation of Membrane Electrode Assembly (MEA)]

As shown in FIG. 7, the gas diffusion electrodes G1 (size: 6.0 cm×5.5cm) obtained in the above description and gas separators 17 and 18 addedwith gas flow passages were arranged on both surfaces of the MEA 14obtained in the above description. Moreover, such a body thus obtainedwas sandwiched by stainless steel-made current collectors (not shown)subjected to gold plating, whereby a single cell as an objective ofevaluation was formed. Note that, in FIG. 7, reference numeral 11denotes the solid polymer electrolyte membrane, reference numeral 12denotes the anode catalyst layer, reference numeral 13 denotes thecathode catalyst layer, reference numerals 15 and 16 denote the gasdiffusion electrodes, reference numeral 17 denotes the anode-sideseparator, reference numeral 18 denotes the cathode-side separator,reference numeral 19 denotes the fuel gas flow passage, and referencenumeral 20 denotes the oxidizing agent gas flow passage.

Next, hydrogen was supplied as fuel to the anode side of the single cellas the objective of evaluation, and air was supplied as the oxidizingagent to the cathode side thereof. Supply pressures of both of the gaseswere set at the atmospheric pressure. With regard to the hydrogen, atemperature was set at 58.6° C., and a relative humidity was set at 60%.With regard to the air, a temperature was set at 54.8° C., and arelative humidity was set at 50%. A cell temperature was set at 70° C.Moreover, a utilization ratio of the hydrogen was set at 67%, and autilization ratio of the air was set at 40%. A cell voltage in the caseof generating power at a current density of 1.0 A/cm² under suchconditions was measured as an initial cell voltage.

Subsequently, after the power was generated for 60 seconds, this powergeneration was stopped. After the power generation was stopped, thesupply of the hydrogen and the air was stopped, substitution wasperformed for the single cell by using the air, and the single cell wasmade to be on standby for 50 seconds. Thereafter, the hydrogen gas wassupplied to the anode side for 10 seconds at a utilization ratio of 1/5of the above-described utilization ratio. Thereafter, the hydrogen gasand the air were supplied to the anode side and the cathode side,respectively, under similar conditions to those of the abovedescription, and the power was generated again for 60 seconds at acurrent density of 1.0 A/cm². Moreover, a load current at this time wasincreased from 0 A/cm² to 1 A/cm² for 30 seconds. Such powergeneration/stop operations were implemented, and the cell voltage wasmeasured, whereby the power generation performance was evaluated. Thenumber of cycles at the point of time when the cell voltage at thecurrent density of 1.0 A/cm² became 0.45 V was used as an evaluationvalue of the durability. Configurations and results are shown in FIG. 8Aand FIG. 8B.

EXAMPLE 2

In a similar way to Example 1, gas diffusion electrodes G2 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 20:80, and a porosity was 72%.

EXAMPLE 3

In a similar way to Example 1, gas diffusion electrodes G3 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 40:60, and a porosity was 70%.

EXAMPLE 4

In a similar way to Example 1, gas diffusion electrodes G4 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 50:50, and a porosity was 70%.

EXAMPLE 5

In a similar way to Example 1, gas diffusion electrodes G5 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 70:30, and a porosity was 69%.

EXAMPLE 6

In a similar way to Example 1, gas diffusion electrodes G6 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 0.5 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 30:70, and a porosity was 80%.

EXAMPLE 7

In a similar way to Example 1, gas diffusion electrodes G7 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 0.5 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 50:50, and a porosity was 78%.

EXAMPLE 8

In a similar way to Example 1, gas diffusion electrodes G8 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.5 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 30:70, and a porosity was 63%.

EXAMPLE 9

In a similar way to Example 1, gas diffusion electrodes G9 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 1.5 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 50:50, and a porosity was 62%.

EXAMPLE 10

In a similar way to Example 1, gas diffusion electrodes G10 wereobtained, which supported a gas diffusion electrode material in which acoated amount was 2.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 30:70, and a porosity was 54%.

EXAMPLE 11 1. Preparation of Cathode Electrode Catalyst

As the conductive carbon material, 4.0 g of carbon black (Ketjen Black™EC made by Ketjen Black International Company, BET specific surfacearea: 800 m²/g) was prepared. To this conductive carbon material, addedwas 400 g of a dinitrodiammine platinum solution (Pt concentration:1.0%), and a resultant solution was stirred for one hour. Moreover, 50 gof methanol was mixed as a reducing agent to the solution, and aresultant solution was stirred for one hour. Thereafter, the solutionwas heated up to 80° C. for 30 minutes, was stirred at 80° C. for sixhours, and was then cooled down to the room temperature for one hour.After a deposition was filtered, a solid material thus obtained wasdried at 85° C. under a reduced pressure for 12 hours, and was milled inthe mortar, whereby a cathode electrode catalyst (average particlediameter of Pt particles: 2.6 nm; supported concentration of Pt: 50 mass%) was obtained.

2. Fabrication of Cathode Catalyst Layer

Purified water of which amount was five times a mass of the cathodeelectrode catalyst was added thereto, and a resultant solution wassubjected to the decompression/deaerating operation for five minutes.n-propyl alcohol of which amount was 0.5 time an amount of the solutionwas added thereto, and further, a solution (containing 20% Nafion madeby DuPont Corporation) containing a proton-conductive polymerelectrolyte was added thereto. As the polymer electrolyte in thesolution, one was used, in which a solid mass ratio of a content withrespect to the carbon of the cathode electrode catalyst, thatCarbon/Ionomer was equal to 1.0/0.9.

Mixed slurry thus obtained was dispersed well by the ultrasonichomogenizer, and was subjected to the decompression/deaeratingoperation, whereby catalyst slurry was prepared. This catalyst slurry ofwhich amount corresponded to the desired thickness was printed on onesurface of a polytetrafluoroethylene sheet by the screen printingmethod, and was dried at 60° C. for 24 hours. A size of the formedcathode catalyst layer was set at 5 cm×5 cm. Moreover, the coated layeron the polytetrafluoroethylene sheet was adjusted so that an amount ofPt could be 0.4 mg/cm² (average thickness of the cathode catalyst layer:12 μm).

3. Fabrication of Membrane Electrode Assembly (MBA)

The Nafion™ NRE211 (the former NE111) (membrane thickness: 25 μm), whichserved as a solid polymer electrolyte membrane, and the anode electrodecatalyst layer fabricated in Example 1 and the above-described cathodeelectrode catalyst layer were superposed on one another. In this case,the anode catalyst layer, the solid polymer electrolyte membrane and thecathode catalyst layer were stacked on one another in this order.Thereafter, this body thus stacked was hot-pressed at 130° C. and 2.0MPa for 10 minutes, and only the polytetrafluoroethylene sheets werepeeled therefrom, whereby an MEA was obtained.

With regard to the cathode catalyst layer transferred onto the solidpolymer electrolyte membrane, the thickness was approximately 12 μm, thesupported amount of Pt was 0.4 mg per 1 cm² of an apparent electrodearea, and the electrode area was 25 cm². With regard to the anodecatalyst layer, the thickness was approximately 6 nm, the supportedamount of Pt was 0.2 mg per 1 cm² of an apparent electrode area, and theelectrode area was 25 cm².

This MEA was combined with the gas diffusion electrodes G1 fabricated inExample 1, and evaluation was performed therefor.

EXAMPLE 12

An MEA was evaluated in a similar way to Example 1 except for usingcarbon black (Vulcan XC-72) made by Cabot Corporation in place of theacetylene black (AB-6) made by Denki Kagaku Kogyo Kabushiki Kaisha inthe case of fabricating the gas diffusion electrode material of Example1.

EXAMPLE 13

An MEA was evaluated in a similar way to Example 1 except for using thecarbon black (Ketjen Black™ EC) made by Ketjen Black InternationalCompany in place of the acetylene black (AB-6) made by Denki KagakuKogyo Kabushiki Kaisha in the case of fabricating the gas diffusionelectrode material of Example 1.

EXAMPLE 14

An MEA was evaluated in a similar way to Example 1 except for using thegraphitized Ketjen Black in place of the acetylene black (AB-6) made byDenki Kagaku Kogyo Kabushiki Kaisha in the case of fabricating the gasdiffusion electrode material of Example 1.

EXAMPLE 15

The gas diffusion electrode materials A1 fabricated in Example 1 werecut out into a predetermined size (6.0 cm×5.5 cm), and were superposedon both surfaces of the MEA fabricated in advance in Example 1.

In this case, the gas diffusion electrode material A1, the MEA (oneformed by stacking and bonding the anode catalyst layer, the solidpolymer electrolyte membrane and the cathode catalyst layer in thisorder) and the gas diffusion electrode material A1 were stacked on oneanother in this order.

Thereafter, this body thus stacked was subjected to the bondingtreatment for three minutes at 130° C. and 2 MPa by the hot press.Pieces of the carbon paper (6.0 cm×5.5 cm) were superposed on one thusobtained, in which the gas diffusion electrode materials were arrangedon both sides of the MEA. Then, such a body thus obtained was used forthe evaluation.

Comparative Example 1

3 g of the surfactant (Triton X-100 made by The Dow Chemical Company)and 200 g of the pure water were mixed together, and a resultantsolution was subjected to the stirring treatment for 30 minutes at 150rpm in the propeller stirrer. Thereafter, 20 g of the acetylene black(AB-6) made by Denki Kagaku Kogyo Kabushiki Kaisha was put into andmixed with the above-described surfactant-dispersed solution, and aresultant mixture was subjected to the stirring treatment for 30 minutesat 150 rpm in the propeller stirrer.

The above-described ink slurry was subjected to the milling treatment byusing the jet mill, and an average particle diameter of carbon thereofwas set at 1 μm. 15 g of the Polyflon D-1E (solid content: 64%) made byDaikin Industries, Ltd. was put into and mixed with the above-describedink slurry. Then, a resultant mixture was subjected to the stirringtreatment for 30 minutes at 150 rpm in the propeller stirrer, andfurther, was subjected to the decompression/deaerating operation,whereby slurry was obtained.

This slurry of which amount corresponded to the desired thickness wasprinted by the screen printing method on one surface of the carbon papernamed TGP-H060 made by Toray Industries, Inc., which had a size of 10 cmsquare, and was dried at 80° C. for 24 hours. Thereafter, the slurry andthe carbon paper were subjected to the heat treatment for 30 minutes inthe heating furnace (at the air atmosphere) at 350° C., and thePTFE-dispersed particles in the slurry were molten, and were dispersedonto the carbon particles, whereby the gas diffusion electrode materialwas formed. In such a way, a gas diffusion electrode g1 was obtained,which had a gas diffusion layer (a porous layer (a mill layer)) in whicha coated amount was 2.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 30:70, and a porosity was 40%.

Bonded bodies of the gas diffusion electrodes g1 thus obtained were cutout into a predetermined size (6.0 cm×5.5 cm), were combined with theMEA of Example 1, and evaluation was performed therefor.

Comparative Example 2

As shown in FIG. 3, a base material with a size of 10 cm square was cutout of a polytetrafluoroethylene porous membrane sheet in which athickness was 50 μm, a pore diameter ranged from 0.5 to 45 μm (anaverage pore diameter: 15 μm), and a porosity was 60%. Incidentally,FIG. 3A shows a surface region of the porous membrane, and FIG. 3B showsan intermediate region thereof.

In a similar way to Example 1, this polytetrafluoroethylene porousmembrane sheet was allowed to contain the ink slurry, whereby a gasdiffusion electrode material was fabricated.

In a similar way to Example 1, gas diffusion electrodes G16 wereobtained, which supported the gas diffusion electrode material in whicha coated amount was 1.0 mg/cm², a mass ratio of (PTFE): (Conductor) wasequal to 30:70, and a porosity was 40%. FIG. 4 shows photographs of across section of the gas diffusion electrode G16.

Comparative Example 3

The gas diffusion electrodes G16 of Comparative example 2 were combinedwith the MEA fabricated in Example 11, and evaluation was performedtherefor.

EXAMPLE 16 [Fabrication of Gas Diffusion Electrode] 1. Preparation ofPolytetrafluoroethylene Porous Membrane

A PTFE porous thin membrane with an average particle diameter of 10 μmand a thickness of 50 μm was cut to a square of 10 cm.

2. Preparation of Hydrophilizing Treatment Solution

5 g of the surfactant (Triton X-100 made by The Dow Chemical Company)and 200 g of ethanol were mixed together, and a resultant solution wassubjected to stirring/dispersion treatment for 30 minutes at 150 rpm inthe propeller stirrer, and was formed into a hydrophilizing treatmentsolution.

3. Preparation of Coating Ink Slurry

3 g of the surfactant (Triton X-100 made by The Dow Chemical Company)and 200 g of pure water were mixed together, and a resultant solutionwas subjected to stirring treatment for 30 minutes at 150 rpm in thepropeller stirrer. Thereafter, 20 g of carbon black (Vulcan XC-72R madeby Cabot Corporation) was put into and mixed with the above-describedsurfactant-dispersed solution, and a resultant mixture was subjected tostirring treatment for 30 minutes at 150 rpm in the propeller stirrer.

The above-described ink slurry was subjected to milling treatment byusing the jet mill, and an average particle diameter of carbon thereofwas set at 1 μm. 13 g of the Polyflon D-1E made by Daikin Industries,Ltd. was put into and mixed with the above-described ink slurry. Then, aresultant mixture was subjected to stirring treatment for 30 minutes at150 rpm in the propeller stirrer, whereby coating ink slurry was formed.

4. Hydrophilizing Treatment of PTFE Porous Membrane

The PTFE porous membrane prepared in Step 1 was fixed to the stainlesssteel-made jig in which a hollow portion had a size of 8 cm square, andwas immersed into the hydrophilizing treatment solution prepared in Step2, followed by decompression and suction.

5. Coating of Ink Slurry

Before being completely dried, the PTFE porous membrane subjected to thehydrophilizing treatment in Step 4 was immersed into the ink slurryprepared in Step 3, followed by decompression and suction, and was driedin the drying furnace at 70 to 100° C.

6. Heating of PTFE Porous Membrane

The PTFE porous membrane on which the ink slurry was coated in Step 5was subjected to heating treatment for 20 minutes in the heating furnaceat 320° C., whereby a gas diffusion electrode material was formed.

Note that, in the obtained gas diffusion electrode material, the massratio of (PTFE): (Conductor) was equal to 30:70.

7. Bonding of PTFE Porous Membrane

The above-described gas diffusion electrode material was set on carbonpaper (TGP-H-060 made by Toray Industries, Inc.) with a size of 10 cmsquare, and the gas diffusion electrode material and the carbon paperwere subjected to boding treatment by the hot press.

8. Cutting of Gas Diffusion Electrode

A set of the carbon paper and the gas diffusion electrode material,which was obtained in Step 7, was cut out to a predetermined size,whereby a gas diffusion electrode was formed.

[Evaluation of Gas Diffusion Electrode]

As shown in FIG. 7, the membrane electrode assembly (MEA) 14 sandwichedby such obtained gas diffusion electrodes 15 and 16 was sandwiched bythe separator 17 having the gas flow passage 19 and by the separator 18having the oxidizing agent gas flow passage 20, whereby a single cell ofa fuel cell was assembled.

Under the atmospheric pressure, the hydrogen gas and the air wereintroduced into the anode electrode and the cathode electrode,respectively. Then, the single cell was subjected to aging treatment forthree hours at a cell temperature of 70° C. and a load current densityof 1 A/cm². Thereafter, power generation performance of the cell wasevaluated.

When Examples 1 to 16 and Comparative example 1 are compared with eachother, it is understood that the MEA using the gas diffusion layers(GDLs) in each of which the gas diffusion electrode materials of thepresent invention are supported on the carbon paper is more excellent inperformance and durability in comparison with the MEA using theconventional gas diffusion layers (GDLs).

Moreover, when Examples 1 to 16 are compared with Comparative examples 2and 3, in the case of Comparative examples 2 and 3, the density of themicrofiber does not largely differ between the intermediate region andthe surface region as shown in FIGS. 3A and 3B, and accordingly, theparticles of the conductive material are held at substantially the samedensity in the intermediate region and the surface region as shown inFIG. 4. Therefore, it is considered that the performance and durabilityof these Comparative examples are decreased in comparison with the gasdiffusion electrode of the present invention since the drainage in theelectrode catalyst layers is decreased, and the movement of the waterheld in the electrolyte membrane is inhibited.

The entire contents of Japanese Patent Application No. 2005-281141(filed on Sep. 28, 2005) and Japanese Patent Application No. 2006-46126(filed on Feb. 23, 2006) are incorporated herein by reference.

The description has been made above of the contents of the presentinvention along the embodiments and the examples. However, it isself-evident to those skilled in the art that the present invention isnot limited to the descriptions of these, and that various modificationsand improvements are possible.

INDUSTRIAL APPLICABILITY

In accordance with the present invention, the polytetrafluoroethylenehaving the predetermined three-dimensional structure was used, and soon. Therefore, it is possible to provide the gas diffusion electrodematerial excellent in power generation characteristics and durability,to provide the production method thereof, and to provide the gasdiffusion electrode thereof.

1. A method for producing a gas diffusion electrode material,comprising: hydrophilizing a porous body formed ofpolytetrafluoroethylene microfibers and having three-dimensionallycontinuous micropores; impregnating and adhering slurry containing aconductive material into and onto the hydrophilized porous body; andperforming heat treatment for the porous body onto which the conductivematerial is adhered.
 2. The method for producing a gas diffusionelectrode material according to claim 1, further comprising: fabricatingthe porous body by stretching a polytetrafluoroethylene membrane.
 3. Themethod for producing a gas diffusion electrode material according toclaim 1, wherein, in the hydrophilizing the porous body, ahydrophilizing treatment solution which contains surfactant and anorganic solvent having hydrophilic groups is filled into the microporesof the porous body.
 4. The method for producing a gas diffusionelectrode material according to claim 1, wherein, in the adhering theslurry, the slurry is brought into contact with either a front surfaceor back surface of the porous body, and the slurry is subsequentlyimpregnated into the porous body by pressurization or decompression,followed by drying under a normal atmospheric pressure.
 5. The methodfor producing a gas diffusion electrode material according to claim 4,wherein the slurry is brought into contact with either one surface of afront surface or back surface of the porous body, the slurry issubsequently impregnated into the porous body, followed by drying,thereafter, the slurry is brought into contact with the other surface ofthe porous body, and the slurry is subsequently impregnated into theporous body by pressurization or decompression, followed by drying underthe normal atmospheric pressure.
 6. The method for producing a gasdiffusion electrode material according to claim 1, wherein, in theperforming heat treatment, the heat treatment is performed at atemperature ranging from 300 to 400° C.
 7. The method for producing agas diffusion electrode material according to claim 1, wherein, in theperforming heat treatment, for the porous body onto which the conductivematerial is adhered, the heat treatment is performed in a state wheretension is applied to the porous body in a direction parallel to thesurface of the porous body.
 8. The method for producing a gas diffusionelectrode material according to claim 1, wherein a density of thepolytetrafluoroethylene microfibers is lower in a surface region of across section of the porous body than in an intermediate region of thecross section of the porous body.